CN104260940A - Ozone water concentration stabilization constant voltage system of beverage-packaging production line - Google Patents

Ozone water concentration stabilization constant voltage system of beverage-packaging production line Download PDF

Info

Publication number
CN104260940A
CN104260940A CN201410533160.2A CN201410533160A CN104260940A CN 104260940 A CN104260940 A CN 104260940A CN 201410533160 A CN201410533160 A CN 201410533160A CN 104260940 A CN104260940 A CN 104260940A
Authority
CN
China
Prior art keywords
ozone water
water
ozone
beverage
pipeline
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN201410533160.2A
Other languages
Chinese (zh)
Other versions
CN104260940B (en
Inventor
李永锋
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
CHINA GREAT WALL GRAPE WINE Co Ltd
Original Assignee
CHINA GREAT WALL GRAPE WINE Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by CHINA GREAT WALL GRAPE WINE Co Ltd filed Critical CHINA GREAT WALL GRAPE WINE Co Ltd
Priority to CN201410533160.2A priority Critical patent/CN104260940B/en
Publication of CN104260940A publication Critical patent/CN104260940A/en
Application granted granted Critical
Publication of CN104260940B publication Critical patent/CN104260940B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65BMACHINES, APPARATUS OR DEVICES FOR, OR METHODS OF, PACKAGING ARTICLES OR MATERIALS; UNPACKING
    • B65B55/00Preserving, protecting or purifying packages or package contents in association with packaging
    • B65B55/02Sterilising, e.g. of complete packages
    • B65B55/04Sterilising wrappers or receptacles prior to, or during, packaging
    • B65B55/10Sterilising wrappers or receptacles prior to, or during, packaging by liquids or gases
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65BMACHINES, APPARATUS OR DEVICES FOR, OR METHODS OF, PACKAGING ARTICLES OR MATERIALS; UNPACKING
    • B65B2210/00Specific aspects of the packaging machine
    • B65B2210/06Sterilising or cleaning machinery or conduits

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)

Abstract

The invention relates to the technical field of beverage-packaging production line sterilization, in particular to an ozone water concentration stabilization constant voltage system of a beverage-packaging production line. At present, when the beverage-packaging production line stops working, an ozonator does not work and ozone water concentration in pipelines decreases; after the beverage-packaging production line is started, the concentration of the ozone water entering a washer cannot increase to the sterilization concentration instantly, and accordingly the sterilization for liquid beverage bottles is not thorough. The ozone water concentration stabilization constant voltage system is composed of a softened water supply system, an ozone water mixing system and an ozone water constant voltage constant current system. A softened water tank is connected with a water pump, an outlet of the water pump is connected with an inlet of a filter vat, and an outlet of the filter vat is connected with a four-way valve disposed at the bottom of an ozone water blending tank. The high-pressure water pump is connected with the four-way valve disposed at the bottom of the ozone water blending tank, and the outlet end of the high-pressure water pump is connected with a steam water mixing system. An ozonator is connected onto a pipeline through a jet device, and the high-pressure water pump and the steam water mixing system are connected onto the pipeline, too. The ozone water blending tank is connected with the ozone water constant voltage constant current system. The ozone water constant voltage constant current system is also connected with the beverage-packaging production line and the softened water tank.

Description

Beverage filling production lines consistency of ozone water stablizes constant-voltage system
Technical field
The present invention relates to beverage filling production lines sterilization technology field, a kind of beverage filling production lines consistency of ozone water stablizes constant-voltage system specifically.
Background technology
At present, when the Ozone Water mixed system of liquid beverage canning line runs and controls with bottle placer is chain, when not having burgundy bottle to enter filling flushing, canning line is in run-stopping status, now ozone generator does not work, and ducted consistency of ozone water can reduce immediately; After canning line starts, the consistency of ozone water entering blast cleaner can not rise to bacteriocidal concentration at once, causes liquid beverage bottle sterilization not thorough, affects finished beverage quality.In addition, because ozone dissolves extremely unstable in water, hydraulic pressure, temperature, water consumption etc. are created a great impression to concentration value, therefore, keep beverage filling production lines consistency of ozone water to stablize constant voltage extremely important.
Summary of the invention
The object of this invention is to provide a kind of beverage filling production lines consistency of ozone water and stablize constant-voltage system, to overcome the defect that prior art exists.
Technical scheme of the present invention is by softening water water supply system, Ozone Water mixed system, and Ozone Water constant pressure and flow system forms;
Softening water water supply system comprises softening tank, water pump, filter vat; Softening tank is connected to filter vat entrance by water pump, and filter basket outlet port is connected to water inlet bottom Ozone Water mixing can through pipeline;
Ozone Water mixed system comprises oxygenerator, ozone generator, high-pressure hydraulic pump, Ozone Water mixing can, ejector and ozone concentration on-line computing model; Oxygenerator is connected to ozone generator admission port through flow counter (flow is controllable), and ozone generator outlet is through pipeline and pneumatic stopping valve, check valve connection ejector admission port; Bottom Ozone Water mixing can, four way valve is housed, connects high-pressure hydraulic pump import, filter basket outlet port pipeline, sluicing valve respectively; High-pressure hydraulic pump water outlet is connected with ejector water inlet, and ejector water outlet is connected to Ozone Water mixing can top through pipeline; High-pressure hydraulic pump, ejector, Ozone Water mixing can composition circulating line;
Ozone Water constant pressure and flow system comprises Ozone Water reflux line, towards filling blast cleaner pipeline, blowdown valve, electromagnetic valve, electromagnetic valve; Ozone Water reflux line one end connects and leads to filling blast cleaner pipeline, and one end connects softening tank, reflux line is equipped with blowdown valve, electromagnetic valve A; Connect Ozone Water mixing can top towards filling blast cleaner pipeline one end, one end connects filling blast cleaner, and pipeline is provided with electromagnetic valve B.
Further, described Ozone Water mixing can top is provided with thief hatch (for consistency of ozone water value in ozone concentration on-line computing model monitoring mixing can).
Further, bottom described Ozone Water mixing can, sluicing valve is housed.
Further, 0.45 micron-sized filter stick is housed in described filter vat.
The invention has the beneficial effects as follows that the high-concentrated ozone from ozone generator is dissolved in softening water by Ozone Water mixing can.After dissolving mixing, form the ozone sterilization water of even concentration.By being installed at the consistency of ozone water on-line computing model on mixing can exit end, can the concentration value of Real-Time Monitoring Ozone Water.The constant pressure and flow system of pipe outlet makes a part of Ozone Water be delivered to the use of filling blast cleaner, exceed part Ozone Water and be back to softening tank, ensure ozone generator continuous working, can effectively for canning line provides the ozone sterilization water of constant pressure, constant density value.
Accompanying drawing explanation
Fig. 1 is system schematic of the present invention.
Detailed description of the invention
In figure: 1. softening tank, 2. water pump, 3. filter vat, 4, sluicing valve 5. Ozone Water mixing can, 6. on-line computing model, 7. high-pressure hydraulic pump, 8. ejector, 9. check valve, 10. pneumatic stopping valve, 11. ozone generators, 12. flow counter, 13. oxygenerators, 14. blowdown valves, 15. electromagnetic valve A, 16. electromagnetic valve B.
As can be seen from Figure 1, the present invention by softening water water supply system, Ozone Water mixed system, Ozone Water constant pressure and flow system form;
Softening water water supply system comprises softening tank 1, water pump 2, filter vat 3; Softening tank 1 connects filter vat 3 entrance by water pump 2, and filter vat 3 exports and connects water inlet bottom Ozone Water mixing can 5 by pipeline;
Ozone Water mixed system comprises oxygenerator 13, ozone generator 11, high-pressure hydraulic pump 7, Ozone Water mixing can 5, ejector 8 and ozone concentration on-line computing model 6; Oxygenerator 13 connects ozone generator 11 admission port by flow counter 12, and ozone generator 11 exports and connects ejector 8 admission port by pipeline and pneumatic stopping valve 10, check valve 9; Bottom Ozone Water mixing can 5, four way valve is housed, connects high-pressure hydraulic pump 7 import, filter vat 3 outlet conduit, sluicing valve 4 respectively; High-pressure hydraulic pump 7 water outlet is connected with ejector 8 water inlet, and ejector 8 water outlet is connected to Ozone Water mixing can 5 top through pipeline; High-pressure hydraulic pump 7, ejector 8, Ozone Water mixing can 5 form circulating line;
Ozone Water constant pressure and flow system comprises Ozone Water reflux line, towards filling blast cleaner pipeline, blowdown valve 14, electromagnetic valve 15, electromagnetic valve 16; Ozone Water reflux line one end connects and leads to filling blast cleaner pipeline, and one end connects softening tank 1, reflux line is equipped with blowdown valve 14, electromagnetic valve A15; Connect Ozone Water mixing can 5 top towards filling blast cleaner pipeline one end, one end connects filling blast cleaner.
Described Ozone Water mixing can 5 top is provided with thief hatch.
Bottom described Ozone Water mixing can 5, sluicing valve 4 is housed.
0.45 micron-sized filter stick is housed in described filter vat 3.
Obviously, the above embodiment of the present invention is only for example of the present invention is clearly described, and is not the restriction to embodiments of the present invention.For those of ordinary skill in the field, can also make other changes in different forms on the basis of the above description.Here cannot give exhaustive to all embodiments.Every belong to technical scheme of the present invention the apparent change of extending out or variation be still in the row of protection scope of the present invention.

Claims (4)

1. beverage filling production lines consistency of ozone water stablizes a constant-voltage system, it is characterized in that by softening water water supply system, Ozone Water mixed system, and Ozone Water constant pressure and flow system forms;
Softening water water supply system comprises softening tank (1), water pump (2), filter vat (3); Softening tank (1) connects filter vat (3) entrance by water pump (2), and filter vat (3) outlet connects Ozone Water mixing can (5) bottom water inlet by pipeline;
Ozone Water mixed system comprises oxygenerator (13), ozone generator (11), high-pressure hydraulic pump (7), Ozone Water mixing can (5), ejector (8) and ozone concentration on-line computing model (6); Oxygenerator (13) connects ozone generator (11) admission port by flow counter (12), and ozone generator (11) outlet is by pipeline and pneumatic stopping valve (10), check valve (9) connection ejector (8) admission port; Four way valve is equipped with in Ozone Water mixing can (5) bottom, connects high-pressure hydraulic pump (7) import, filter vat (3) outlet conduit, sluicing valve (4) respectively; High-pressure hydraulic pump (7) water outlet is connected with ejector (8) water inlet, and ejector (8) water outlet is threaded a pipe and connected Ozone Water mixing can (5) top; High-pressure hydraulic pump (7), ejector (8), Ozone Water mixing can (5) composition circulating line;
Ozone Water constant pressure and flow system comprises Ozone Water reflux line, towards filling blast cleaner pipeline, blowdown valve (14), electromagnetic valve (15), electromagnetic valve (16); Ozone Water reflux line one end connects and leads to filling blast cleaner pipeline, and one end connects softening tank (1), reflux line is equipped with blowdown valve (14), electromagnetic valve A(15); Connect Ozone Water mixing can (5) top towards filling blast cleaner pipeline one end, one end connects filling blast cleaner, and pipeline is provided with electromagnetic valve B(16).
2. a kind of beverage filling production lines consistency of ozone water as claimed in claim 1 stablizes constant-voltage system, it is characterized in that Ozone Water mixing can (5) top is provided with thief hatch.
3. a kind of beverage filling production lines consistency of ozone water as claimed in claim 1 stablizes constant-voltage system, it is characterized in that sluicing valve (4) is equipped with in described Ozone Water mixing can (5) bottom.
4. a kind of beverage filling production lines consistency of ozone water as claimed in claim 1 stablizes constant-voltage system, it is characterized in that, in described filter vat (3), 0.45 micron-sized filter stick is housed.
CN201410533160.2A 2014-10-11 2014-10-11 Beverage filling production lines consistency of ozone water is stablized constant-voltage system Active CN104260940B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410533160.2A CN104260940B (en) 2014-10-11 2014-10-11 Beverage filling production lines consistency of ozone water is stablized constant-voltage system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410533160.2A CN104260940B (en) 2014-10-11 2014-10-11 Beverage filling production lines consistency of ozone water is stablized constant-voltage system

Publications (2)

Publication Number Publication Date
CN104260940A true CN104260940A (en) 2015-01-07
CN104260940B CN104260940B (en) 2016-05-18

Family

ID=52152574

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201410533160.2A Active CN104260940B (en) 2014-10-11 2014-10-11 Beverage filling production lines consistency of ozone water is stablized constant-voltage system

Country Status (1)

Country Link
CN (1) CN104260940B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112357147A (en) * 2020-10-20 2021-02-12 北京圣祥乳制品厂 A water liftout device for dairy products filling equipment

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0222309A1 (en) * 1985-11-11 1987-05-20 Consiglio Nazionale Delle Ricerche Method for sanitizing packaging containers and materials, particularly for pharmaceutical and cosmetics use, and plant for implementing the method
JPH0356222A (en) * 1989-07-26 1991-03-11 Toyo Seikan Kaisha Ltd Dry sterilizing method for germfree filling container
CN2263097Y (en) * 1994-11-06 1997-09-24 陈明震 Adjustable automatic quantitative liquid filling device
CN1868860A (en) * 2006-06-26 2006-11-29 山东新华医疗器械股份有限公司 Constant pressure filling system
CN101044098A (en) * 2004-08-24 2007-09-26 光彩服务有限公司 Water purification apparatus
CN201966095U (en) * 2010-12-28 2011-09-07 平顶山市联立机电有限公司 Thermostatic constant-voltage air charging device of diaphragm capsule for temperature controller
CN204161683U (en) * 2014-10-11 2015-02-18 中国长城葡萄酒有限公司 Beverage filling production lines consistency of ozone water stablizes constant-voltage system

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0222309A1 (en) * 1985-11-11 1987-05-20 Consiglio Nazionale Delle Ricerche Method for sanitizing packaging containers and materials, particularly for pharmaceutical and cosmetics use, and plant for implementing the method
JPH0356222A (en) * 1989-07-26 1991-03-11 Toyo Seikan Kaisha Ltd Dry sterilizing method for germfree filling container
CN2263097Y (en) * 1994-11-06 1997-09-24 陈明震 Adjustable automatic quantitative liquid filling device
CN101044098A (en) * 2004-08-24 2007-09-26 光彩服务有限公司 Water purification apparatus
CN1868860A (en) * 2006-06-26 2006-11-29 山东新华医疗器械股份有限公司 Constant pressure filling system
CN201966095U (en) * 2010-12-28 2011-09-07 平顶山市联立机电有限公司 Thermostatic constant-voltage air charging device of diaphragm capsule for temperature controller
CN204161683U (en) * 2014-10-11 2015-02-18 中国长城葡萄酒有限公司 Beverage filling production lines consistency of ozone water stablizes constant-voltage system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112357147A (en) * 2020-10-20 2021-02-12 北京圣祥乳制品厂 A water liftout device for dairy products filling equipment
CN112357147B (en) * 2020-10-20 2022-07-12 北京圣祥乳制品厂 A water liftout device for dairy products filling equipment

Also Published As

Publication number Publication date
CN104260940B (en) 2016-05-18

Similar Documents

Publication Publication Date Title
JP2017509464A5 (en)
CN103047539B (en) Chemical liquor supply system
KR101261316B1 (en) Device and method for pipe-cleaning using fine-bubble
RU2015145735A (en) VENTILATION SYSTEM FOR NUCLEAR INSTALLATION HAZARD
DE16842406T1 (en) PROCESS FOR CLEANING A LIQUID
CN207811449U (en) A kind of oxygen-dissolving apparatus
CN204161683U (en) Beverage filling production lines consistency of ozone water stablizes constant-voltage system
CA2960082A1 (en) Apparatus and method for dispensing a wash solution for conveying the same into a washing device, car wash facility and program media
CN104260940A (en) Ozone water concentration stabilization constant voltage system of beverage-packaging production line
CN206356334U (en) A kind of transverse tube type coal gas primary cooler tube bank cleaning device
CN105251739A (en) Cleaning technology for sterilization system
CN211411652U (en) Alkali dissolving and online adding system thereof
CN205133460U (en) Emulsion explosive's emulsification pharmacy system
CN205056577U (en) System for wash and thoughtlessly glue aircraft nose pipeline
CN203904667U (en) Brand new bleaching and dyeing device
CN102553473A (en) Water and gas blender
JP2015191972A5 (en)
CN204368111U (en) A kind of rearmounted foam water inlet car washing installation
CN204567599U (en) For the water tank of self-service carwash
CN203833648U (en) Chemical feeding device for sewage treatment system
CN203979888U (en) Acid solution feeding mechanism during a kind of PCB produces
CN207547135U (en) Semiconductor slice equipment cleaning solution co-feeding system
CN204247033U (en) Flush of hydrogen gas tower cleaning solution recycling system
CN208916955U (en) The reverse osmosis unit of concentrated water recycling speeder
CN208679030U (en) A kind of automatic releasing agent proportioning system

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant